Fuel storage and supply arrangement having fuel conditioning and filtration system

ABSTRACT

A fuel storage and supply arrangement serving as a source of fuel to be dispensed via at least one fuel dispenser in a fuel dispensing environment. The arrangement comprises a storage tank for containing a quantity of the fuel and a pump assembly for drawing the fuel from the storage tank providing the fuel under pressure. A fuel supply line is configured to convey the fuel under pressure from the pump assembly to the at least one fuel dispenser in a dispenser flow path. A fuel conditioning and filtration assembly comprise a housing having a housing inlet receiving the fuel under pressure created by the pump and a housing outlet whereby the fuel entering the housing inlet exits the housing through the housing outlet. A filter element is within the housing and interposed in the flow path between the housing inlet and the housing outlet. A return tube receiving fuel from the outlet of the housing is also provided. An agitator manifold receiving the fuel from the return tube and having an agitator tube defining a plurality of agitation holes, the agitator tube being positioned proximate to the bottom of the fuel storage tank. In addition, the agitator manifold is movable between an insertion orientation and a deployed orientation. A flow control valve is provided for controlling the flow of the fuel along the fuel conditioning and filtration flow path.

FIELD OF THE INVENTION

The present invention relates generally to fuel dispensing environmentshaving one or more fuel storage tanks. More particularly, the presentinvention relates to a fuel dispensing environment in which one or moreof the storage tanks are equipped with a fuel conditioning andfiltration assembly.

BACKGROUND

Fuel dispensing environments, such as retail fueling stations and fueldepots, typically store fuel in fuel tanks, such as an undergroundstorage tank (UST). In some instances, small amounts of water or debrismay be introduced into the storage tank, which can degrade the fuel. Forexample, during periods of rain, water typically flows over pavement inthe forecourt region of a service station into a storm drain.Occasionally, some of this water may make its way into an undergroundstorage tank. Generally, water and debris are denser than the fuelstored in the tank and thus settle near the bottom of the tank. Waterand fuel are immiscible, which causes a water layer to form below thefuel creating a fuel/water interface layer in the storage tank. Thelevel of the fuel/water interface is typically monitored to ensure thatwater is not introduced into the inlet through which fuel is drawn fromthe tanks.

Moreover, the fuel/water interface in the storage tank may besusceptible to colonization and growth of microbial bacteria. Forexample, when storing ultra-low sulfur diesel (ULSD) fuel and/or ULSDblended with biodiesel fuel products, hydrocarbon utilizing microbes,e.g., “humbugs,” may develop. These microbes can foul fuel deliverysystems and ancillary components, including fuel dispenser components,metering devices, shear valves, and fuel nozzles. In addition to thedirect effects of microbial growth, acid byproducts may be generated asa result of microbial digestion of food sources found in the ULSD andbiodiesel fuels. These acids attack the metal surfaces in the fuelstorage and delivery systems, which may lead to various problems.

Costly active measures can be taken to clean a contaminated tank, removewater and polish the fuel. This method requires shutting the tank down,which adds an additional cost of lost sales to the already high cost ofcleaning. This process typically involves making multiple passes of thetank contents through progressively restrictive filter media and,ultimately, through a coalescing filter that removes any free water.These cleaning systems are large scale, typically truck mounted and aredesigned to clean up contamination as opposed to preventingcontamination.

Many passive means are utilized to prevent or detect entrance of waterinto fuel tanks, such as vent line caps, inlet seals, tank inspections,and regular quality testing. However, even small amounts of water maycause serious degradation of the fuel tank and/or fuel. When water isdetected, the entirety of the storage tank may need to be pumped in tosetting tanks to have the water drained. After the water is drained, thefuel may then be reintroduced to the storage tank. Alternatively, thefuel tank may be allowed to settle and a suction hose is used to drawout water at the bottom of the fuel tank until the water layer isremoved and only fuel flows through the suction hose.

SUMMARY OF CERTAIN ASPECTS

The present invention recognizes and addresses the foregoingconsiderations, and others, of prior art construction and methods. Inthis regard, certain exemplary and nonlimiting aspects of the presentinvention will now be described. These aspects are intended to providesome context for certain principles associated with the presentinvention, but, are not intended to be defining of the full scope of thepresent invention.

In an example embodiment of the present invention, a compact fuelconditioning and filtration assembly (FCFA) provides ongoingconditioning and filtering of fuel by removing water and debris from thebottom of a fuel storage tank, such as a UST. The removal of water anddebris from the UST may directly improve the cleanliness and quality ofthe fuel dispensed therefrom. Further, the FCFA may limit or preventcolonization and growth of microbial bacteria that can develop at thefuel/water interface layer in the UST and prevent development ofhydrocarbon utilizing microbes, e.g., “humbugs,” that can foul fueldelivery systems and ancillary components. Additionally, since microbesare prevented from growing by removal of the water, the FCFA alsoreduces or eliminates the acid byproducts that result from the microbe'sdigestion of food sources (e.g., in ULSD and biodiesel fuels), therebylimiting or preventing acid damage to the metal surfaces of the fuelstorage and delivery systems.

The FCFA may be fluidly coupled to a submersible turbine pump (STP)associated with a UST. The STP provides fuel flow through a manifold toone or more fuel dispensers either continuously or on demand. In thisregard, the FCFA may be fluidly coupled to a test or bypass port of apacker manifold associated with the STP. As the fuel flows through themanifold, a portion of the fuel, which is relatively small compared tothe fuel flow to the fuel dispenser, may be diverted through the testport to the FCFA and back to the UST after filtration. In an exampleembodiment, the FCFA may be disposed in an existing STP containment sumpprovided at the fuel dispensing site.

The FCFA may include a filter element configured to remove water fromthe fuel flowing therethrough. For example, the filter element maydefine a flow path, which allows or encourages water to precipitate tothe bottom the filter element due to the density of water being greaterthan the density of the fuel. Additionally, debris may also precipitateout of the fuel toward the bottom of the filter element or be otherwisecaptured by filter media.

The FCFA may include one or more control valves to control the flow offuel through the filter element and/or allow for draining of waterand/or debris from the filter element to a storage reservoir. Forexample, a flow control valve may be disposed in the flow path of thefuel from the manifold through the filter element, and back to the UST.When the flow control valve is closed, fuel is prevented from flowingthrough the FCFA. At desired intervals and/or times, the flow controlvalve may be opened to allow flow of fuel through the FCFA. In this way,the operation of the FCFA may be limited to only the necessary durationto condition and filter the fuel and avoid periods when the fueldispensers are more active. This may prevent or limit any impact tofueling operation caused by the diversion of a portion of the fuelthrough the FCFA. At the completion of one or more conditioning andfiltering processes, e.g., when the flow control valve is closed, adrain valve disposed at or near the bottom of the filter housing may beopened to allow water and/or debris to flow into a storage reservoir.Collecting the water in this manner may extend the in-service period ofthe FCFA between maintenance operations. Moreover, collecting water inthis manner proportionately reduces the amount of water available tomobilize microbial colonies in a manner that as the total surface areaof the fuel/water interface is reduced, the microbial bacteria has lessand less access to food sources in the fuel.

In some embodiments, the FCFA may include a return tube in fluidcommunication with the filter outlet. The return tube may be configuredto cause turbulent flow at the bottom of the UST. The turbulent flow maycause water and debris near the bottom of the UST to mix with the fueland therefore be more likely to enter, i.e., be drawn into, the inlet ofthe STP. In some embodiments, a diffuser (agitation manifold) defining aplurality of spaced apertures may be fluidly connected to the distal endof the return tube to cause turbulent flow over a wider area at thebottom of the UST.

One aspect of the present invention provides a fuel storage and supplyarrangement serving as a source of fuel to be dispensed via at least onefuel dispenser in a fuel dispensing environment. The arrangementcomprises a storage tank for containing a quantity of the fuel. A pumpassembly is operative to draw the fuel from the storage tank into thefuel piping. A fuel supply line is configured to convey fuel from thefuel storage tank to the at least one fuel dispenser. A fuelconditioning and filtration assembly (FCFA) includes a housing having ahousing inlet receiving the fuel under pressure created by the pumpassembly and a housing outlet whereby the fuel entering the housinginlet exits the housing through the housing outlet. A filter elementlocated within the housing is interposed in the flow path between thehousing inlet and the housing outlet, the filter element beingconfigured to remove water from the fuel passing through the filterelement. The FCFA also includes a return tube receiving fuel from theoutlet of the housing and having a discharge end disposed proximate to abottom of the storage tank such that fuel flowing through the returntube causes turbulence in the fuel at the bottom of the storage tank.The flow of fuel to the housing inlet of the housing and through thedischarge end of the return tube defines a fuel conditioning andfiltration flow path. The FCFA also includes a flow control valvecontrolling the flow of fuel the through the fuel conditioning andfiltration flow path.

Another aspect of the present invention provides a method ofconditioning and filtering fuel including providing a fuel conditioningand filtration assembly comprising an inlet in fluid communication withfuel piping, wherein the fuel piping is configured to convey fuel from afuel storage tank to one or more fuel dispensers. An outlet is in thefuel storage tank to return the fuel. A filter element is interposedalong a flow path between the inlet and the outlet, wherein the filterelement is configured to remove water from the fuel passing through thefilter element. A flow control valve disposed in the flow path allowsand prevents flow of fuel through the filter element. The method furtherincludes determining, by processing circuitry, if pressure dataassociated with the fuel piping or a number of active fuel dispensersassociated with the fuel storage tank satisfies a predeterminedoperation criteria. In addition, the method includes causing the flowcontrol valve to open in response to the pressure data or the number ofactive fuel dispensers satisfying the predetermined operation criteria.

A still further aspect of the present invention provides a fuelconditioning and filtration assembly for use with a fuel storage tankproviding fuel to at least one fuel dispenser via fuel piping fed with afuel pump. The assembly comprises an inlet in fluid communication withthe fuel piping. An outlet in the fuel storage tank returns the fuel. Afilter interposed along a flow path between the inlet and the outlet isconfigured to remove water from the fuel passing through the filter. Aflow control valve disposed in the flow path allows and prevents flow offuel through the filter. A storage reservoir in fluid communication withthe filter is configured to receive water drained from the filter. Aconductivity sensor configured to measure conductivity of fluid withinthe filter is also provided. A drain valve is operatively disposedbetween the filter and the storage reservoir. Processing circuitry isoperative to control the flow control valve based on predeterminedoperation criteria, the processing circuitry being further configured toreceive conductivity data from the conductivity sensor, determine ifwater is present in the filter based on the conductivity data, and causethe drain valve to open if water is present allowing the water to drainfrom the filter to the storage reservoir.

A further aspect of the present invention provides a fuel storage andsupply arrangement serving as a source of fuel to be dispensed via atleast one fuel dispenser in a fuel dispensing environment. Thearrangement comprises a storage tank for containing a quantity of thefuel and a pump assembly for drawing the fuel from the storage tankproviding the fuel under pressure. A fuel supply line is configured toconvey the fuel under pressure from the pump assembly to the at leastone fuel dispenser in a dispenser flow path. A fuel conditioning andfiltration assembly comprises a housing having a housing inlet receivingthe fuel under pressure created by the pump assembly and a housingoutlet whereby the fuel entering the housing inlet exits the housingthrough the housing outlet. A filter element is within the housing andinterposed in the flow path between the housing inlet and the housingoutlet. A return tube receiving fuel from the outlet of the housing isalso provided. An agitator manifold receives the fuel from the returntube and has an agitator tube defining a plurality of agitation holes,the agitator tube being positioned proximate to the bottom of the fuelstorage tank. In addition, the agitator manifold is movable between aninsertion orientation and a deployed orientation. A flow control valveis provided for controlling the flow of the fuel along the fuelconditioning and filtration flow path.

In an exemplary embodiment, the agitator manifold comprises rigid firstand second tube portions interconnected for flow by a flexible tube, thesecond tube portion forming the agitator tube. Preferably, the secondtube portion is substantially axially aligned with the first tubeportion in the insertion orientation and is substantially perpendicularto the first tube portion in the deployed orientation. In some cases,the diametric extent of the agitator manifold in the insertionorientation is less than 4 inches.

A linkage assembly may be provided to effect movement of the agitatormanifold into the deployed orientation. For example, the linkageassembly may comprise a handle linkage and an agitator linkageinterconnected by at least one interconnecting bar (such as first andsecond interconnecting rods). The handle linkage may also comprise arotatable bar structure pivotally connected with respect to the firsttube portion. Moreover, the handle linkage may include a removablehandle. A removable pin may extend through the rotatable bar structureto maintain the second tube portion in the deployed orientation.

In some exemplary embodiments, the agitator linkage comprises at leastone L-shaped bar having a shorter bar portion and a longer bar portion.The at least one L-shaped bar in such embodiments may be pivotallyconnected to the first tube portion at the intersection of the shorterbar portion and the longer bar portion. For example, the at least oneL-shaped bar may be pivotally connected to the first tube portion via anaxially extending arm that is fixed to the first tube portion. Moreover,the interconnecting bar is pivotally connected to the at least oneL-shaped bar adjacent a distal end of the shorter bar portion.

Another aspect of the present invention provides an agitator manifoldfor use with a fuel recirculation system. The agitator manifoldaccording to this aspect comprises rigid first and second tube portionsinterconnected for flow by a flexible tube, the second tube portionforming an agitator tube defining a plurality of agitation holes. Thefirst and second tube portions are movable between an insertionorientation in which the second tube portion is substantially axiallyaligned with the first tube portion and a deployed orientation in whichthe second tube portion is substantially perpendicular to the first tubeportion. A deployment linkage assembly effects movement of the agitatormanifold into the deployed orientation.

An additional aspect of the present invention provides a method ofinstalling an agitation tube in an underground storage tank having aninsertion opening of predetermined diameter. One step of the methodinvolves providing an agitator manifold having rigid first and secondtube portions interconnected for flow by a flexible tube, the secondtube portion forming an agitator tube defining a plurality of agitationholes. The first and second tube portions are movable between aninsertion orientation in which the second tube portion is axiallyaligned with the first tube portion and a deployed orientation in whichthe second tube portion is substantially perpendicular to the first tubeportion. A deployment linkage assembly effects movement of the agitatormanifold into the deployed orientation.

According to another step of the method, the agitator manifold, in theinsertion orientation, is inserted into the underground storage tank viathe insertion opening such that the second tube portion is completelyinside the underground storage tank and the first tube portion is onlypartially inside the underground storage so that the linkage assemblycan be accessed. The deployment linkage assembly is utilized to move thesecond tube portion into the deployed orientation and the linkageassembly is fixed so as to maintain the deployed orientation. Theagitator manifold assembly is moved so that the first tube portion islocated completely inside the underground storage tank and the secondtube portion is located substantially parallel to a bottom of theunderground storage tank.

Different systems and methods of the present invention utilize variouscombinations of the disclosed elements and method steps as supported bythe overall disclosure herein. Thus, combinations of elements other thanthose discussed above may be claimed. Moreover, the accompanyingdrawings, which are incorporated in and constitute a part of thisspecification, illustrate one or more embodiments of the invention and,together with the description, serve to explain the principles of theinvention.

BRIEF DESCRIPTION OF THE DRAWINGS

A full and enabling disclosure of the present invention, including thebest mode thereof directed to one of ordinary skill in the art, is setforth in the specification, which makes reference to the appendeddrawings, in which:

FIG. 1 is a diagrammatic representation of a fuel storage arrangementhaving a fuel conditioning and filtration assembly in accordance with anembodiment of the present invention.

FIG. 2 is a detailed diagrammatic representation of certain aspects of afuel conditioning and filtration assembly in accordance with anembodiment of the present invention.

FIG. 3 is a block diagram of one example of processing circuitryaccording to an example embodiment.

FIGS. 4-6 illustrate example methods for conditioning and filtering fuelaccording to an example embodiment.

FIG. 7 is a diagrammatic representation of a fuel storage arrangementhaving a fuel conditioning and filtration assembly in accordance withanother embodiment of the present invention.

FIG. 8 is a detailed diagrammatic representation of certain aspects of afuel conditioning and filtration assembly in accordance with anotherembodiment of the present invention.

FIG. 9 is a side elevation of an agitator manifold in accordance with anembodiment of the present invention in a deployed orientation.

FIG. 10 is perspective view of the agitator manifold of FIG. 10 in aninstallation (insertion) orientation.

FIGS. 10A through 10C are enlarged views of the portions of the agitatormanifold in FIG. 10 so indicated.

FIG. 11A is an enlarged perspective view of a handle linkage utilized inthe agitator manifold of FIG. 9.

FIG. 11B is a right side elevation of the handle linkage utilized in theagitator manifold of FIG. 9.

FIG. 11C is a left side elevation of the handle linkage utilized in theagitator manifold of FIG. 9.

FIG. 12A is an enlarged perspective view of an agitator linkage utilizedin the agitator manifold of FIG. 9.

FIG. 12B is a right side elevation of the agitator linkage utilized inthe agitator manifold of FIG. 9.

FIG. 12C is a left side elevation of the agitator linkage utilized inthe agitator manifold of FIG. 9.

FIG. 13 is an enlarged side elevation of a portion of the agitatormanifold of FIG. 9 including the handle linkage and the agitator linkageof the deployment linkage assembly.

FIG. 14 is an enlarged fragmentary side elevation showing the handlelinkage in the deployed orientation.

FIG. 15 is an enlarged fragmentary side elevation showing the agitatorlinkage in the deployed orientation.

FIG. 16 is a flowchart showing certain exemplary steps of methodology inaccordance with an aspect of the present invention.

DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS

Reference will now be made in detail to presently preferred embodimentsof the invention, one or more examples of which are illustrated in theaccompanying drawings. Each example is provided by way of explanation ofthe invention, not limitation of the invention. In fact, it will beapparent to those skilled in the art that modifications and variationscan be made in the present invention without departing from the scope orspirit thereof. For instance, features illustrated or described as partof one embodiment may be used on another embodiment to yield a stillfurther embodiment. Thus, it is intended that the present inventioncovers such modifications and variations as come within the scope of theappended claims and their equivalents.

FIG. 1 shows a fuel storage and supply system 100 with a fuel storagetank 110, such as an underground storage tank (UST), which stores aquantity of fuel 10 to be dispensed by fuel dispensers 150 in a fueldispensing environment, such as a retail fueling station. A tank probe160 extends into the storage tank 110, and has a fuel level sensor 161for determining the level of fuel 10 in the storage tank 110 and a waterlevel sensor 162 for determining the level of water 20 (and anycontaminants therein) in the storage tank 110. A fuel pump, such as pumpassembly 130 in the depicted embodiment, is associated with the storagetank 110 to pump the fuel 10 into fuel supply lines 140 for providingthe fuel 10 to the one or more fuel dispensers 150. The path that thefuel 10 flows from the fuel pump to the fuel dispensers 150 is thedispenser flow path. The fuel dispensers 150 will have a dispenser fuelmeter 151 to monitor the dispensing of fuel 10 by the respective fueldispensers 150, and the fuel supply lines 140 may have one or more linepressure sensor(s) 141 (FIG. 2).

In embodiment illustrated, the pump assembly 130 includes a pump 131,such as a submersible turbine pump (STP), immersed in the fuel 10 at thelower end of a column 132. A packer manifold 134, defining a main fluidpassageway and a number of ports, is located at the upper end of thecolumn 132. The pump 131 sends the fuel 10, and sometimes water 20, fromthe tank 110 through the column 132 to the packer manifold 134 foraccess at the ports in the packer manifold 134. One of these ports, apump outlet 135, supplies the fuel supply lines 140. A check valve 133is located along the fluid passageway of the pump assembly 130 betweenthe pump 131 and the pump assembly outlet 135, to retain fuel 10 underpressure in the fuel supply lines 140 when dispensing is not occurringand pump 131 is off. As one skilled in the art will appreciate, thepacker manifold 134 will typically be located in a containment sump 120defined below ground level when the storage tank 110 is a UST. Oneskilled in the art will understand and appreciate that, althoughillustrated as a submersible turbine pump, the pump 131 may be anyconfiguration that draws fuel 10 from the storage tank 110. One exampleof pump 131 is a Red Jacket submersible turbine pump sold by Veeder-RootCompany of Simsbury, Conn.

An automatic tank gauge (ATG) 190 manages the storage and supply of fuel10 in the fuel storage and supply system 100. (Suitable ATGs include theTLS-450 ATG and the TLS-350 ATG sold by Veeder-Root Company.) The ATG190 is electrically connected to the tank probe 160 to determine thelevel of fuel 10 and water 20 in the tank 110. The ATG 190 is alsoelectrically connected to the fuel dispenser meters 151 in the fueldispensers 150 (or otherwise to control circuitry for the fueldispensers 150) and to the pump 131. The ATG 190 is also in electricalcommunication with the pressure sensor(s) 141.

Using information received from the fuel dispenser meters 151 and thepressure sensor 141, the ATG 190 can operate the pump 131 to satisfy theneeds of the fuel dispensers 150. Moreover, the ATG 190 can use the linepressure sensor 141 to detect potential leaks in the fuel supply lines140. Specifically, the ATG 190 can use the pump 131 to pressurize thefuel supply lines 140 during a dormant period when the fuel dispensersare not dispensing fuel 10. Once the fuel supply lines 140 arepressurized, the ATG 190 turns off the pump 131 and monitors thepressure in the supply lines with the line pressure sensor 141. Becauseof the check valve 133 in the pump assembly 130, the fuel supply lines140 should maintain pressure for a predetermined period. If the ATG 190determines that the pressure in the fuel supply lines 140 decreased toomuch or too quickly, there is an indication of a leak somewhere in thefuel storage and supply system 100, most likely in the fuel supply lines140. The line pressure sensor 141 used to measure pressure in the fuelsupply line 140 may be disposed at any point in the fuel supply line 140between the pump 131 and a fuel dispenser 150, such as the outlet of thepacker manifold 134.

In the present invention, a fuel conditioning and filtration assembly(FCFA) 200 is provided to improve the cleanliness and quality of thefuel 10 in the storage tank 110 by removing water 20 and anycontaminants in the water. The FCFA 200 receives fuel 10, and water 20when present, removed from the storage tank 110 by the pump assembly130, and returns that fuel 10 to the storage tank after filtering outthe contaminants and water 20.

In the embodiment illustrated in FIG. 2, FCFA 200 has a fuelconditioning and filtration element 212, or filter element, thatseparates the contaminants and water 20 from the fuel 10. Filter element212 is located in a housing 211 having a housing inlet 211 a and ahousing outlet 211 b. (Together, housing 211 and filter element 212 maybe referred to herein as a filter.) Housing inlet 211 a is in fluidcommunication with the dispenser flow path to receive at least some fueldrawn from tank 110 by the pump assembly 130. In this embodiment, forexample, housing inlet 211 a is in fluid communication with a port 136provided in packer manifold 134. (The connection to port 136 can thus beconsidered an “inlet” for the overall FCFA.) Port 136 may be an existingport on packer manifold 134 otherwise provided, for example, for testpurposes. Housing outlet 211 b is in fluid communication with thestorage tank 110. The housing 211 can also include a drain outlet 211 cfor removal of the contaminate and water 20 filtered out of the fuel 10by the filter element 212.

The filter element 212 is preferably a water separation (coalescing)filter that is capable of separating free and emulsified water 20 fromthe fuel 10 flowing therethrough while also removing other contaminantsfrom the fuel 10. The use of the FCFA 200 is particularly advantageousfor fuel storage and supply systems 100 that store ultra-low sulfurdiesel (ULSD) fuel and/or ULSD blended with biodiesel fuel products. Asdiscussed above, hydrocarbon utilizing microbes, e.g., “humbugs,” maydevelop in storage tanks, such as USTs, at or near the fuel/waterinterface. By removing the contaminants and water, not only is thequality of the fuel improved, but the microbe development may beprevented or limited.

Referring again to FIG. 1, an agitation return 220 returns the fuel fromthe FCFA 200 to the storage tank 110. (The discharge end of theagitation return in the storage tank is considered the outlet for theFCFA.) The agitation return 220 is fluidly connected to the housingoutlet 211 b of housing 211 and extends to the interior of the storagetank 110. In a preferred embodiment, the agitation return 220 dischargesproximate to the bottom of the storage tank 110. Discharge of the fuel10 in this manner desirably causes turbulence in the fuel 10 near thebottom of the storage tank 110. As noted above, contaminants and/orwater 20 tend to collect at or near the bottom of the storage tank 110because of their density. The turbulence thus causes the contaminantsand/or water 20 to be mixed into the bulk of the fuel 10, which may,thereby, be accessible to the pump 131.

In an example embodiment, agitation return 220 may comprise a returntube 221 with a discharge end 222 proximate to a bottom of the storagetank 110. The discharge end 222 of the return tube can also supply anagitator manifold 232 that is elongated across a portion of the bottomof the storage tank 110. As shown, agitator manifold 232 defines aplurality of agitator apertures 233 at least some of which arepreferably directed towards the bottom of the storage tank 110. Forexample, the agitator manifold can be in the form of an elongate tube, aseries of parallel tubes, a circle, a rectangle, a plurality of tubesextending from a central point in a “star pattern,” or any othersuitable configuration, with the agitator apertures 233 being spacedtherealong. The returning fuel 10 is thus discharged through theagitator apertures 233 of the agitator manifold 232 causing turbulencenear the bottom of the tank 110 across a larger area than simpledischarge at the end of return tube 221. This turbulence facilitatesmixing of the water 20 and/or debris (contaminants) in the fuel 10. Thesuspended water 20 and/or debris may then become entrained in the fuel10 as it is drawn into the pump 131. This enables the water 20 anddebris to be actively removed by the FCFA 200, reducing or eliminatingthe need to remove the storage tank from service in order to removewater and/or debris. Additionally, a separate particle filter can alsobe added to the fuel flow path, preferably before the filter element212, in order to extend its service life.

The FCFA 200 includes a fuel flow control valve 230 disposed at anysuitable location in the flow path back to the storage tank 110. In thisembodiment, valve 230 is located in the flow path of the fuel downstreamfrom the housing outlet 211 b. Embodiments are contemplated, however, inwhich the valve 230 is upstream of the housing inlet 211 a (i.e.,between port 136 and housing inlet 211 a). The fuel flow control valve230 may be any suitable remotely operated valve, such as a solenoidvalve, a servo-actuated valve, a hydraulically actuated valve, or thelike. As described in more detail below, the flow control valve 230 maybe opened periodically to allow flow through the FCFA 200 and closed toprevent flow through the FCFA 200.

As shown in FIG. 2, processing circuitry (controller) 400 is utilized tocontrol operation of the flow control valve 230 and other aspects ofFCFA 200. In this regard, the processing circuitry 400 may provide asignal (or otherwise control power supplied) to the actuator of the flowcontrol valve 230. This will cause the valve 230 to open or close, whichwill allow or prevent flow of fuel 10 through the FCFA 200. It isanticipated that the processing circuitry 400 may be a standalone unit,or alternatively can be a part of other processors or controllers, suchas the ATG 190. For example, the firmware of ATG 190 can be updated toprovide the additional functionality described herein.

In the embodiment illustrated, FCFA 200 also includes a flow resistancedetector, such as a pressure differential sensor 240, to determine theoperational state of filter element 212. In this regard, the filterelement 212 may experience a buildup of debris and become inefficient ornon-functional while in operation. The buildup of debris and loss ofefficiency to the filter element 212 may be indicated by a change in thedifferential pressure across the filter element 212. The processingcircuitry 400 can monitor the pressure differential sensor 240 todetermine the need for replacing the filter element 212. For example,the processing circuitry 400 may periodically (such as once per minute,once per second, once per program loop, etc.) compare differentialpressure data received from the pressure differential sensor 240 to apredetermined differential pressure. When the processing circuitry 400determines that the differential pressure deviates from thepredetermined differential pressure, the processing circuitry 400 causesa filter service request to be generated and transmitted to the ATG 190or other remote computing device. Additionally, if the processingcircuitry 400 determines that the differential pressure across thefilter element 212 exceeds the predetermined differential pressure, theprocessing circuitry 400 can prevent the flow control valve 230 of theFCFA 200 from opening, therefore preventing flow through the FCFA 200.

A water sensor 250 can also be positioned within the FCFA 200 todetermine the presence of water 20 that has been removed by the filterelement 212. In one embodiment, the water sensor 250 comprises aconductivity sensor that utilizes a change of state or conductivity,e.g., due to the difference in resistance between the water and fuel, todetermine whether water is present. However, any type of suitable watersensor can be used that one skilled in the art will understand canperform the desired function. Preferably, the water sensor 250 would bepositioned at a location in relation to filter element 212 where waterwill collect, such as at the bottom of housing 211.

In the embodiment illustrated, a storage reservoir assembly 300 is usedto collect the contaminants and water 20 filtered from the fuel 10 toextend the time between maintenance operations. The storage reservoirassembly 300 includes a storage reservoir 310 that has a storagereservoir inlet 311 in fluid communication with the drain outlet 211 cof the housing 211. A reservoir drain valve 320, positioned between thedrain outlet 211 c of the housing 211 and the storage reservoir inlet311, controls the flow of contaminants and water 20 into the storagereservoir 310. The reservoir drain valve 320 may be any suitableremotely operated valve, such as a solenoid valve, a servo-actuatedvalve, a hydraulically actuated valve, or the like. The processingcircuitry 400, being also in communication with the water sensor 250,can activate the reservoir drain valve 320 when water 20 in the housing211 is above the desired level. As a result, fluid in the housing 211will be caused to flow through the drain outlet 211 c and into thestorage reservoir 310 through the storage inlet 311. Embodiments arecontemplated in which reservoir 310 is integrated with housing 211.

A reservoir level sensor 330 can be used to determine the level of water20 in the storage reservoir 310, which can then be removed through adrain 312 in the storage reservoir 310. In one embodiment, the reservoirlevel sensor 330 is a conductivity sensor that utilizes a change ofstate or conductivity, e.g., due to the difference in resistance todetect the presence of water 20 at a specific level. However, any typeof suitable level sensor can be used that one skilled in the art willunderstand can perform the desired function.

The reservoir level sensor 330 is preferably connected to the processingcircuitry 400, which may verify that sufficient volume is available inthe storage reservoir 310 prior to causing the drain valve 320 to open.If sufficient volume is available, as indicated by the fluid level(volume) being below a fill threshold, the processing circuitry 400causes the drain valve 320 to open. If sufficient volume is notavailable, as indicated by the fluid level being above the fillthreshold, the processing circuitry 400 may maintain the drain valve 320in the closed position despite the indication of presence of water 20 inthe housing 211 as indicated by the water sensor 250. When theprocessing circuitry 400 determines that the fluid level in the storagereservoir 310 is above the fill threshold, the processing circuitry 400can cause a service request to be generated and transmitted to the ATG190 or other remote computing device. Additionally, if the processingcircuitry 400 determines that the fluid level in the storage reservoir310 is above the fill threshold, the processing circuitry 400 canprevent the flow control valve 230 of the FCFA 200 from opening,therefore preventing flow through the fuel conditioning and filtrationflow path.

In some example embodiments, the processing circuitry 400 can beconfigured to open the flow control valve 230 and operate the FCFA 200when the water level sensor 162 reaches a predetermined level. Theprocessing circuitry 400 can also be configured to prevent the operationof the FCFA 200 when the water level sensor 162 indicates a level ofwater 220 below a predetermined level. Moreover, the processingcircuitry 400 may be configured to limit impact on fueling operations,such as allowing the FCFA 200 to be in service when there is low or nodispensing activity in the fuel dispensing environment. For example, theprocessing circuitry 400 may be configured to place the FCFA 200 inservice, by opening flow control valve 230, during times of day thattypically have little or no fueling operations (such as 12:00 AM). Inone embodiment, the controller 400 thus determines that a current timesatisfies a predetermined operation time and causes the flow controlvalve 230 to open. If the pump 130 is not already activated, it will becaused to activate by processing circuitry 400 in order to force fuelthrough FCFA 200.

The controller 400 may also operate the FCFA 200 based on predeterminedoperation criteria, such as pressure in the fuel line 140 and/or thenumber of active fuel dispensers 150 associated with the storage tank110. For example, the processing circuitry 400 may receive an indicationfrom the ATG 190 of the number of active fuel dispensers. Moreover, theprocessing circuitry 400 may receive from the ATG 190 pressure dataindicating the pressure measured by the line pressure sensor 141 in thefuel supply line 140.

To facilitate the determination of when to operate FCFA 200, theprocessing circuitry 400 may include one or more lookup tables definingrelevant operation thresholds (e.g., based on the power rating anddischarge size of the pump 131 associated with one or more storage tanks110). For example, Table 1 below provides operation thresholds for TankNos. 1-4 in an exemplary fuel dispensing environment, each with adifferent pump and discharge configuration.

TABLE 1 Max. # of Fuel Min. Tank # Pump/Discharge Type DispensersPressure 1 1.5 HP, 2″ Discharge 4 25 psi 2 5 HP, 4″ Discharge 10 30 psi3 2 × 2 HP, 2″ Discharge with IPC 8 25 psi 4 Generic Pump 3 20 psi

In this embodiment, the processing circuitry 400 compares the actualpressure data and/or the actual number of active fuel dispensers 150 totheir respective operation thresholds defined in the look-up table. Ifthe pressure data is less than the minimum threshold and/or the activenumber of fuel dispensers 150 is equal to or greater than the maximum,the predetermined operation criteria is not satisfied. In this event,the processing circuitry 400 may then close the flow control valve 230(or keep it closed). If, however, the pressure data and/or the number ofactive fuel dispensers 150 satisfies their respective operation criteria(depending on whether or not both criteria are required), the processingcircuitry 400 may cause opening of the flow control valve 230. Further,if the flow control valve 230 is open at the time of determination thatan operation threshold is not satisfied, the processing circuitry 400causes the flow control valve 230 to close.

In addition, or in the alternative, the processing circuitry 400 may beconfigured to place the FCFA 200 in service for a selected duration,such as one hour, two hours, or other suitable time period. In aninstance in which the processing circuitry 400 closes the flow controlvalve 230 prior to the selected duration, such as due to a pressure dropor number of active fuel dispensers 150 exceeding the threshold, theprocessing circuitry 400 may reopen the flow control valve 230 when theoperation criteria is again satisfied to continue the conditioning andfiltration process.

At the beginning of operation, the processing circuitry 400 maydetermine if water is present in the FCFA 200. As discussed above, theprocessing circuitry 400 may receive conductivity data from the watersensor 250 indicative of the presence or absence of water 20 in thehousing 211. In response to the processing circuitry 400 determining anabsence of water 20 in the housing 211, the processing circuitry 400performs conditioning of the fuel 10 by causing the flow control valve230 to open.

In response to the processing circuitry 400 determining that water 20 ispresent in the housing 211, the drain valve 320 is caused to open for asufficient time to allow water 20 in the housing 211 to drain. In anexample embodiment, the processing circuitry 400 may then cause the FCFA200 to be placed back in service for an additional period of time. Theprocess may repeat until the processing circuitry 400 determines anabsence of water in the housing 211 or until the end of the selectedservice duration or until the storage reservoir 310 is full as indicatedby level sensor 330.

Example Processing Circuitry

FIG. 3 shows certain elements of processing circuitry 400 in accordancewith a preferred embodiment. The processing circuitry 400 may be aself-contained unit as noted above, or may be distributed among acombination of devices. For example, the ATG may be programmed toperform the functions described herein, in which case at least someaspects of processing circuitry 400 may comprise components of the ATG.Furthermore, it should be noted that the devices or elements describedbelow may not be mandatory and thus some may be omitted in certainembodiments.

In an example embodiment, the processing circuitry 400 may include orotherwise be in communication with one or more processors 62 (andassociated memory 64). As one skilled in the art will recognize,processor 62 is configured to perform data processing, applicationexecution, and other processing and management services. Processor 62may be in communication with or otherwise control a user interface 66, acommunication interface 68, one or more valves 70, and one or moresensors 72. Processor 62 may be embodied as a circuit chip (e.g., anintegrated circuit chip) configured (e.g., with hardware, software or acombination of hardware and software) to perform operations describedherein. In some embodiments, however, the processor 62 may be embodiedas a portion of a server, computer, or workstation, or distributed amongseveral physical processors.

The user interface 66 may be an input/output device for receivinginstructions directly from a user. The user interface 66 may receiveuser input and/or present output to a user as, for example, audible,visual, mechanical, or other output indications. The user interface 66may include, for example, a keyboard, a mouse, a joystick, a display(e.g., a touch screen display), a microphone, a speaker, or otherinput/output mechanisms.

Communication interface 68 may be any suitable means such as a device orcircuitry embodied in either hardware, software, or a combination ofhardware and software that is configured to receive and/or transmit datafrom/to a network and/or any other device or module in communicationwith the processor 62. As such, for example, communication interface 68may include a communication modem and/or other hardware/software forsupporting communication via Ethernet, digital subscriber line (DSL),universal serial bus (USB), or other suitable mechanisms/protocols. Inan exemplary embodiment, communication interface 68 may supportcommunication via one or more different communication protocols ormethods.

In an example embodiment, the memory 64 may include one or morenon-transitory storage or memory devices such as, for example, volatileand/or non-volatile memory that may be either fixed or removable. Thememory 64 may be configured to store information, data, applications,instructions or the like for enabling the apparatus to carry out variousfunctions in accordance with example embodiments of the presentinvention. For example, the memory 64 could be configured to bufferinput data for processing by the processor 62. Additionally oralternatively, the memory 64 could be configured to store instructionsfor execution by the processor 62. As yet another alternative, thememory 64 may include one of a plurality of databases that may store avariety of files, contents, or data sets. Among the contents of thememory 64, applications may be stored for execution by the processor 62in order to carry out the functionality associated with each respectiveapplication.

Processing circuitry 400 may also be in communication with valves, suchas flow control valve 230 and drain valve 320 discussed above inreference to FIG. 2. The processing circuitry 400 may cause the valves70 to open periodically to allow flow or close the valves 70 to preventflow.

Processing circuitry 400 may also include or be in communication withone or more sensors 72. The sensors 72 may include, without limitation,the line pressure sensor 141, the tank fuel level sensor 161, the tankwater level sensor 162, differential pressure sensor 240, water sensor250, and/or the reservoir level sensor 330, as discussed above inreference to FIG. 2. The sensors 72 may provide sensor data (such asconductivity data, level data, differential pressure data, and/orpressure data) to the processor 62. The processor 62 may utilize thesensor data to determine if one or more conditions or thresholds aresatisfied during the conditioning process.

Example Flowchart(s) and Method(s)

Referring to FIGS. 4-6, methods that may be utilized in accordance withvarious aspects described herein are illustrated. While, for purposes ofsimplicity of explanation, the methods are shown and described as aseries of acts, it is to be understood and appreciated that the methodsare not limited by the order of acts, as some acts may, in accordancewith one or more aspects, occur in a different sequence and/orconcurrently with other acts from that shown and described herein. Forexample, those skilled in the art will understand and appreciate that amethod could alternatively be represented as a series of interrelatedstates or events, such as in a state diagram. Moreover, not allillustrated acts may be required to implement a method in accordancewith one or more aspects. Some optional steps or operations areindicated, for example, by dashed lines. In other words, embodiments arecontemplated in which various steps of the described methodology are notincluded. For example, some embodiments may rely on satisfying pressurecriteria in order to operate without regard to the number of dispensersin use, or vice versa. Other embodiments are contemplated in which thein service time of FCFA 200 is not based on dispensing activity. Forexample, in cases where a fuel dispensing environment is known to beclosed for part of the day, the conditioning and filtration assembly canbe operated only during that time.

As indicated at operation 500 (FIG. 4), the method may start with theprocessing circuitry determining that a current time satisfies apredetermined operation time (e.g., 12:00 AM). Next, the processingcircuitry may receive pressure data associated with the fuel piping atoperation 502 and/or receive an indication of a number of active fueldispensers associated with a fuel storage tank at operation 504. Theprocessing circuitry may then determine if the pressure data and/or thenumber of active fuel dispensers satisfies predetermined operationcriteria at operation 506. If the pressure data or the number of activefuel dispensers fails to satisfy the predetermined operation criteria,the processing circuitry may proceed directly to operation 516 bydiscontinuing the conditioning process (e.g., by closing, or maintainingclosed, the FCFA flow control valve). If the pressure data and/or thenumber of active fuel dispensers satisfies predetermined operationcriteria at operation 506, the method may proceed to operation 508.

At operation 508, the processing circuitry may cause the flow valve toopen in response to the pressure data and/or the number of active fueldispensers satisfying the predetermined operation criteria. Theprocessing circuitry may determine if an operating duration hassatisfied a predetermined conditioning duration at operation 510.Conductivity data from a conductivity sensor is received as indicated atoperation 512. The processing circuitry may determine at operation 514if water is present in a filter based on the conductivity data. If nowater is present, the method proceeds to operation 516, at which theprocessing circuitry discontinues the conditioning process by causingthe flow valve to close. If water is present, the method proceeds tooperation 518 of FIG. 5.

At operation 518, the processing circuitry may suspend the conditioningprocess for a predetermined period of time by closing the flow controlvalve. The processing circuitry may receive level data from a levelsensor associated with a storage reservoir at operation 520 anddetermine if the reservoir level exceeds a predetermined fill thresholdat operation 522. If the level data exceeds the predetermined fillthreshold, the processing circuitry may generate a reservoir servicerequest at operation 524 and then proceed to operation 516 (FIG. 4). Ifthe level data does not exceed the predetermined fill threshold, theprocessing circuitry may cause the drain valve to open to drain waterfrom the filter element to the storage reservoir at operation 526 andcause the drain valve to close in response to the conductivity sensorindicating no water present in the filter at operation 128. The methodmay repeat by returning to operations 502/504, until the processingcircuitry determines that no water is present in the filter element atoperation 514.

Turning to FIG. 6, the method may also include monitoring thedifferential pressure across the filter while the flow valve is open.The processing circuitry may receive differential pressure data from adifferential pressure sensor associated with the filter element atoperation 530 and determine if the differential pressure data differsfrom predetermined criteria at operation 532. In response to determiningthat the differential pressure data differs from predetermined criteria,the processing circuitry may generate a filter service request atoperation 534 and proceed to operation 516 (FIG. 4) discontinuing theconditioning process by closing the flow valve.

FIGS. 7-8 illustrate an alternative FCFA 200′ in accordance with anotherembodiment of the present invention. FCFA 200′ is similar in mostrespects to FCFA 200 described above. Thus, elements of FCFA 200′ thatcorrespond to elements of FCFA 200 will be identified by the samereference number. As will now be described, however, FCFA 200′ has anadditional mode of operation in which vacuum is used to draw water 20from tank 110 in bulk form which can be captured in storage reservoir310 for subsequent drainage. The vacuum source utilized for this purposemay be located in the manifold 134 of the pump 130. In this regard, U.S.Pat. No. 8,636,482, incorporated herein by reference in its entirety forall purposes, describes a suitable siphon cartridge that can be used asthe vacuum source.

As shown, vacuum source 600 is in fluid communication with return tube221 at a location upstream of valve 230 via tubing 602. A valve 604 issituated along tubing 602 to selectively connect or disconnect thevacuum source. In addition, tubing 606 provides fluid communicationbetween housing inlet 211 a and return tube 221 downstream of valve 230.A valve 608 is located along tubing 606 in order to connect ordisconnect the fluid communication provided by tubing 606. In addition,an isolation valve 610 is in this case situated along tubing 612 toprovide fluid communication between port 136 and housing inlet 211 a. Itwill be appreciated that valve 610 should be opened when valve 320 isopened to allow drainage of water into reservoir 310 in order to preventback pressure from impeding the flow.

Like valve 230, valves 604, 608, and 610 may be any suitable remotelyoperated valve, such as a solenoid valve, a servo-actuated valve, ahydraulically actuated valve, or the like. Also like valve 230,embodiments are contemplated in which one or more of these valves areconfigured as piloted check valves controlled by a solenoid valve, whichis in turn in fluid communication with port 136. As will be appreciated,valves 604, 608, and 610 are in electrical communication with and arecontrolled by processing circuitry 400.

When it is desired to remove water in bulk from the bottom of tank 110,valves 230 and 610 are closed while valves 604 and 608 are opened. As aresult, a vacuum is drawn on the filter outlet 211 b of the housing 211.Standing water that has collected at the bottom of the storage tank 110can thus be pulled into the housing 211 where the water and any fuel inthe water is separated. In the illustrated embodiment, the water ispulled into the housing 211 via agitator manifold 232, return tube 221(downstream of valve 230), and tubing 606. (Alternatively, a separatetube may be installed very close to the bottom of the storage tank 110for this purpose.) This bulk water collection mode can be run when theSTP is running for normal station operation or during station quiettimes as determined by the ATG 190 and/or processing circuitry 400.

Removal of the standing water can be determined by processing circuitry400 using signals from ATG 190 (as indicated by the water float 162), bymeasuring the rate that water is coming into the filter housing 211 withthe use of a sensor in the housing, a flow meter, by the frequency ofemptying the water reservoir, or a combination of these options. Once itis determined that the standing water has been removed from the tank110, FCFA 200′ may use a valve (or series of valves) to bleed off thevacuum in the filter housing 211 and then pressurize the filter housing211 with fuel using the pump 130. At this time, valves 230 and 610 areopen with valves 604 and 608 being closed. FCFA 200′ will then operatein a conditioning mode substantially to described above in relation toFIGS. 1-6. As needed or periodically as determined by the controller,both bulk water removal and conditioning modes will be used periodicallyto ensure fuel quality and system efficiency. For example, the bulkwater removal mode could be run prior to the conditioning mode each timethe conditioning mode is to be commenced. Alternatively, or in addition,the FCFA may switch back and forth between bulk water removal andconditioning modes as necessary or desired.

Referring now to FIGS. 9-10, an agitator manifold 900 in accordance withan embodiment of the present invention is shown in deployed andinsertion orientations, respectively. As can be seen in FIG. 9, manifold900 generally has a rigid first tube portion 902 which is vertical inthe deployed orientation and a rigid second tube portion 904 which ishorizontal in the deployed orientation. Both portions 902 and 904 areformed as tubes (e.g., having a circular cross section) configured toconvey liquid. In use, first portion 902 constitutes part of return tube221. Second portion 904 defines a plurality of agitator apertures 233(see FIG. 1). A flexible tube 906 (shown schematically in FIG. 12B)interconnects the flow passages of first tube portion 902 and secondtube portion 904. As one skilled in the art will appreciate, tube 906should be formed of a suitable flexible material that will not degradewhen exposed to fuel, such as nitrile.

As shown in FIG. 10, both portions 902 and 904 are substantially axiallyaligned in the insertion orientation. In addition, components ofmanifold 900 are preferably sized to allow manifold 900 to be insertedinto an insertion opening in a UST. Toward this end, and referring nowbriefly to FIG. 14, the diametric extent D2 of the agitator manifold inthe insertion orientation will preferably be less than the innerdiameter D1 of the UST's insertion hole. In many cases, D1 will be 4inches. Once it is inside the tank, second tube portion 904 can be movedto a horizontal position before it is lowered to its final location nearthe bottom of the tank.

Manifold 900 includes a deployment linkage assembly 908 that allows anoperator to easily move second tube portion 904 into the deployedorientation. Referring now also to FIGS. 10A-10C, deployment linkageassembly 908 has a handle linkage 910 mounted on first tube portion 902and an agitator linkage 912 that interconnects first tube portion 902and second tube portion 904. Handle linkage 910 receives an elongatedhandle 914 that is initially closer to first tube portion 902 (as shownin FIGS. 10 and 10A) when manifold 900 is in the insertion orientation.With handle linkage 910 outside the tank but agitator linkage 912 insidethe tank, the operator pushes handle 914 so as to be substantiallyperpendicular to first tube portion 902. This operates agitator linkage912 to move second tube portion 904 to the deployed orientation. Handlelinkage 910 is then locked (as will be explained more fully below) tomaintain the deployed orientation. Handle 914 is removed and handlelinkage 910 is then moved through the tank opening as second tubeportion 904 is moved into its final position near the bottom of thetank.

Referring now to FIGS. 11A-11C, additional details of handle linkage 910can be most easily explained. As shown, handle linkage 910 includes astationary mount 916 that is attached to the outside of first tubeportion 902. A first bar 918 is here in the form of parallel bar plates918 a and 918 b that are pivotally attached to mount 916 (at pivot 920)on opposite sides of first tube portion 902. The distal end of barplates 918 a and 918 b (i.e., the end opposite the end where handle 914is removably attached) are spaced apart so that they may clear firsttube portion 902 when handle 914 is pushed by the operator. Bar plates918 a and 918 b further define an aligned pair of apertures through whena removable cotter pin 922 extends. Cotter pin 922 may be retained by astandard spilt ring 924 that is received in a transverse bore definednear the distal end of pin 922. Cotter pin 922 is, of course, removedwhen bar 918 is pivoted and reinserted once second tube portion 904 isin the deployed orientation. As shown in FIGS. 13, and 14 cotter pin 922will then be on the other side of first tube portion 902 to prevent bar918 from rotating back (thus maintaining the deployed orientation). Atleast one connector bar interconnects handle linkage 910 and agitatorlinkage 912. In this embodiment, a pair of parallel rods 926 a-b arepivotally connected to respective bar plates 918 a-b at an intermediatelocation between pivot 920 and the aligned apertures that receive pin922.

Referring now to FIGS. 12A-12C, details of agitator linkage 912 can bemost easily explained. As seen most clearly in FIGS. 12B and 12C,agitator linkage 912 includes a stationary mount 928 attached to firsttube portion 902. Mount 928 in this embodiment includes a collar 930from which a pair of parallel arms 932 a-b extend. The lower end offirst tube portion 902 and the upper end of second tube portion 904 haverespective fittings 934 and 936 for connection of the flexible tube 906.If necessary or desired, hose clamps may be used to secure flexible hose906 to the fittings 934 and 936.

A second bar is pivotally attached to mount 928 for operation by handlelinkage 910. In this embodiment, the second bar comprises a pair ofL-shaped bar plates 938 a and 938 b which are fixedly attached to secondtube portion 904 (e.g., by collar 940). As shown, plates 938 a-b eachhave a longer bar portion 942 that is axially aligned with second tubeportion 904 and a shorter bar portion 944 that is transverse to longerbar portion 942. Bar plates 938 a-b are pivotally connected torespective arms 930 a-b at the intersection of longer bar portion 942and shorter bar portion 944 (as indicated at 946). In addition,respective rods 926 a-b are pivotally attached to bar plates 938 a-bnear the distal ends of shorter bar portions 944.

As mentioned above, second tube portion 904 is moved to the deployedorientation by rotating handle linkage 910 such that the aligned holesof plates 918 a-b are on the same side of first tube portion 902 aspivot 920. This pulls up rods 926 a-b, which, due to their pivotalconnection near the distal ends of shorter bar portions 944, causesrotation of the second tube portion 904 by substantially 90 degrees.Handle linkage 910 is then retained by cotter pin 922 as previouslydescribed, thus also retaining second tube portion 904 in the deployedorientation.

FIG. 16 shows methodology in accordance with an aspect of the presentinvention. As shown at step 950, the agitator manifold, in the insertionorientation, is partially inserted through an insertion opening in theUST. As shown at 952, the agitator manifold is moved into the deployedorientation using the deployment linkage assembly as described above. Asshown at 954, the agitator manifold is then moved to its final positionin the tank for use.

In some embodiments, the system may be further configured for additionaloperations or optional modifications. In this regard, in an exampleembodiment, the pump comprises a submersible turbine pump (STP). In anexample embodiment, the fuel condition and filtration flow path receivesthe fuel under pressure from the fuel supply line. In some exampleembodiments, the fuel condition and filtration flow path receives thefuel under pressure from the pump. In an example embodiment, the returntube includes an agitator manifold positioned proximate to the bottom ofthe fuel storage tank, the agitator manifold receiving the fuel from thedischarge end of the return tube and having agitation holes directeddownward toward the bottom of the storage tank. In some exampleembodiments, the flow control valve is positioned in the fuelconditioning and filtering flow path downstream from the filter element.In some example embodiments, the flow control valve is positioned in thefuel conditioning and filtration flow path upstream from the filterelement. In an example embodiment, the fuel storage and supplyarrangement also includes processing circuitry operative to control theflow control valve. In some example embodiments, the filter element isfurther configured to remove debris from the fuel passing through thefilter element.

In an example embodiment, the fuel storage and supply arrangement alsoincludes a differential pressure sensor configured to measure thedifferential pressure across the filter element indicating the conditionof the filter element. In some example embodiments, the differentialpressure sensor generates differential pressure data, and furthercomprises processing circuitry configured to receive differentialpressure data from the differential pressure sensor and to generate afilter service request in response to determining that the differentialpressure data exceeds a predetermined pressure difference.

In an example embodiment, the filter housing includes a drain fordischarging water removed from the fuel by the filter element, and thefuel conditioning and filtration assembly further includes a storagereservoir assembly comprising a storage reservoir and a reservoir valveconnecting the storage reservoir with the drain of the housing. In someexample embodiments, the fuel conditioning and filtering assemblyfurther includes a water sensor in the housing for the filter elementthat generates a water signal indicating water in the housing removedfrom the fuel by the filter element, and processing circuitry receivesthe water signal and opens the reservoir valve. In an exampleembodiment, the storage reservoir assembly further includes a reservoirlevel sensor indicating the level of water in the storage reservoir. Insome example embodiments, the reservoir level sensor generates areservoir level signal indicating a level of water in the reservoir, andprocessing circuitry receives the reservoir level signal and opens thereservoir valve when the water in the reservoir reaches a predeterminedreservoir level.

In some example embodiments, the fuel conditioning and filtrationassembly includes a pressure sensor configured to measure the fuelpressure within the fuel piping. In this case, the processing circuitryis configured to receive pressure data from the pressure sensor,determine if the pressure data satisfies predetermined operationcriteria, and cause the flow valve to open in response to the pressuredata satisfying the predetermined operation criteria. In an exampleembodiment, the processing circuitry is configured to receive anindication of a number of active fuel dispensers associated with thestorage tank, determine if the number of active fuel dispenserssatisfies predetermined operation criteria, and cause the flow valve toopen in response to the number of active fuel dispensers satisfying thepredetermined operation criteria.

It will be appreciated that embodiments of the present invention providecompact and effective fuel conditioning and filtration capability.Various advantages are realized by utilizing the existing fuel pumptypically found at the fuel dispensing site. The system can thus beretrofitted into existing retail and fleet fueling sites. The embodimentdescribed in FIGS. 1 and 2 will work with any site fuel pump such as anSTP. Communication with the ATG uniquely manages the balance and flowrequirements of the pump while also taking into consideration siteoperating conditions, such as low or no dispensing activity, while alsolessening impact to other system test functions, e.g., line leak andtank leak detection.

Many modifications and other embodiments of the invention set forthherein will come to mind to one skilled in the art to which thisinvention pertains having the benefit of the teachings presented in theforegoing descriptions and the associated drawings. Therefore, it is tobe understood that the embodiments of the invention are not to belimited to the specific embodiments disclosed and that modifications andother embodiments are intended to be included within the scope of theinvention. Moreover, although the foregoing descriptions and theassociated drawings describe example embodiments in the context ofcertain example combinations of elements and/or functions, it should beappreciated that different combinations of elements and/or functions maybe provided by alternative embodiments without departing from the scopeof the invention. In this regard, for example, different combinations ofelements and/or functions than those explicitly described above are alsocontemplated within the scope of the invention. Although specific termsare employed herein, they are used in a general sense only and not forpurposes of limitation.

What is claimed is:
 1. A fuel storage and supply arrangement serving asa source of fuel to be dispensed via at least one fuel dispenser in afuel dispensing environment, comprising: a storage tank for containing aquantity of the fuel; a pump assembly for drawing the fuel from thestorage tank providing the fuel under pressure; fuel supply lineconfigured to convey the fuel under pressure from the pump assembly tothe at least one fuel dispenser in a dispenser flow path; a fuelconditioning and filtration assembly comprising: a housing having: ahousing inlet receiving the fuel under pressure created by the pumpassembly; and, a housing outlet whereby the fuel entering the housinginlet exits the housing through the housing outlet; a filter elementwithin the housing and interposed in the flow path between the housinginlet and the housing outlet; a return tube receiving fuel from theoutlet of the housing; an agitator manifold receiving the fuel from thereturn tube and having an agitator tube defining a plurality ofagitation holes, said agitator tube being positioned proximate to thebottom of the fuel storage tank; wherein said agitator manifold ismovable between an insertion orientation and a deployed orientation; aflow control valve controlling the flow of the fuel along the fuelconditioning and filtration flow path.
 2. The fuel storage and supplyarrangement of claim 1, wherein the agitator manifold comprises rigidfirst and second tube portions interconnected for flow by a flexibletube, the second tube portion forming the agitator tube.
 3. The fuelstorage and supply arrangement of claim 2, wherein the second tubeportion is substantially axially aligned with the first tube portion inthe insertion orientation and is substantially perpendicular to thefirst tube portion in the deployed orientation.
 4. The fuel storage andsupply arrangement of claim 3, wherein the diametric extent of theagitator manifold in the insertion orientation is less than 4 inches. 5.The fuel storage and supply arrangement of claim 3, comprising a linkageassembly effect movement of the agitator manifold into the deployedorientation.
 6. The fuel storage and supply arrangement of claim 5,wherein the linkage assembly comprises a handle linkage and an agitatorlinkage interconnected by at least one interconnecting bar.
 7. The fuelstorage and supply arrangement of claim 6, wherein the at least oneinterconnecting bar comprises first and second interconnecting rods. 8.The fuel storage and supply arrangement of claim 5, wherein the handlelinkage comprises a rotatable bar structure pivotally connected withrespect to the first tube portion.
 9. The fuel storage and supplyarrangement of claim 5, wherein the handle linkage includes a removablehandle.
 10. The fuel storage and supply arrangement of claim 9, furthercomprising a removable pin extending through said rotatable barstructure to maintain the second tube portion in the deployedorientation.
 11. The fuel storage and supply arrangement of claim 8,wherein the agitator linkage comprises at least one L-shaped bar havinga shorter bar portion and a longer bar portion.
 12. The fuel storage andsupply arrangement of claim 9, wherein the at least one L-shaped bar ispivotally connected to the first tube portion at the intersection of theshorter bar portion and the longer bar portion.
 13. The fuel storage andsupply arrangement of claim 12, wherein the at least one L-shaped bar ispivotally connected to the first tube portion via an axially extendingarm that is fixed to the first tube portion.
 14. The fuel storage andsupply arrangement of claim 12, wherein the interconnecting bar ispivotally connected to the at least one L-shaped bar adjacent a distalend of the shorter bar portion.
 15. An agitator manifold for use with afuel recirculation system, said agitator manifold comprising: rigidfirst and second tube portions interconnected for flow by a flexibletube, the second tube portion forming an agitator tube defining aplurality of agitation holes; said first and second tube portions aremovable between an insertion orientation in which the second tubeportion is substantially axially aligned with the first tube portion anda deployed orientation in which the second tube portion is substantiallyperpendicular to the first tube portion; and a deployment linkageassembly effect movement of the agitator manifold into the deployedorientation.
 16. The agitator manifold of claim 15, wherein the linkageassembly comprises a handle linkage and an agitator linkageinterconnected by at least one interconnecting bar.
 17. The agitatormanifold of claim 16, wherein the at least one interconnecting barcomprises first and second interconnecting rods.
 18. The agitatormanifold of claim 16, wherein the handle linkage comprises a rotatablebar structure pivotally connected with respect to the first tubeportion.
 19. The agitator manifold of claim 18, wherein the handlelinkage includes a removable handle.
 20. The agitator manifold of claim18, further comprising a removable pin extending through said rotatablebar structure to maintain the second tube portion in the deployedorientation.
 21. The agitator manifold of claim 18, wherein the agitatorlinkage comprises at least one L-shaped bar having a shorter bar portionand a longer bar portion.
 22. The agitator manifold of claim 21, whereinthe at least one L-shaped bar is pivotally connected to the first tubeportion at the intersection of the shorter bar portion and the longerbar portion.
 23. The agitator manifold of claim 22, wherein the at leastone L-shaped bar is pivotally connected to the first tube portion via anaxially extending arm that is fixed to the first tube portion.
 24. Theagitator manifold of claim 22, wherein the interconnecting bar ispivotally connected to the at least one L-shaped bar adjacent a distalend of the shorter bar portion.
 25. The agitator manifold of claim 15,wherein the diametric extent of the agitator manifold in the insertionorientation is less than 4 inches.
 26. A method of installing anagitator tube in an underground storage tank having an insertion openingof predetermined diameter, said method comprising steps of: providing anagitator manifold having: rigid first and second tube portionsinterconnected for flow by a flexible tube, the second tube portionforming an agitator tube defining a plurality of agitation holes; saidfirst and second tube portions being movable between an insertionorientation in which the second tube portion is substantially axiallyaligned with the first tube portion and a deployed orientation in whichthe second tube portion is substantially perpendicular to the first tubeportion; and a deployment linkage assembly effect movement of theagitator manifold into the deployed orientation; inserting said agitatormanifold, in the insertion orientation, into the underground storagetank via the insertion opening such that the second tube portion iscompletely inside the underground storage tank and the first tubeportion is only partially inside the underground storage so that thelinkage can be accessed; utilizing the deployment linkage assembly,moving the second tube portion into the deployed orientation and fixingthe linkage assembly so as to maintain the deployed orientation; andmoving the agitator manifold so that the first tube portion is locatedcompletely inside the underground storage tank and the second tubeportion is located substantially parallel to a bottom of the undergroundstorage tank.